Electrochemical system for storing electricity in metals

ABSTRACT

An electrochemical system for storing electrical energy in metallic material comprises a charging assembly having one or more cathode and anode couples for metal deposition and a discharging assembly having one or more cathodes and spaces amid the cathodes for containing metal anode. The charging assembly and discharging assembly are physically separated allowing independent operation of the charging and discharging facilities and independent scaling of power and energy capabilities. It also allows storage of anode metal material in simple containers separated from the charging and discharging assemblies and thus allows for economical energy storage.

CLAIM OF PRIORITY

This application claims priority to U.S. provisional patent applicationSer. No. 61/870,104, filed on Aug. 26, 2013.

FIELD OF THE INVENTION

This invention relates to electrochemical technologies for electricalenergy storage and particularly relates to metal-air batteries, fuelcells and flow batteries.

BACKGROUND OF THE INVENTION

Electricity storage is an important enabling technology for effectiveuse of renewable energy sources such solar and wind. There are two broadcategories of electricity storage applications based on the duration ofstorage: short durations, from a fraction of second to about one hour,and long durations, from a few hours to ten or hundred of hours. Theshort duration types are typically used for power support to ensure thereliability and quality of electrical power for which there aretechnologies in the early stage of commercial application. Long durationtypes are needed for applications to separate the times betweengeneration and use of electricity at low cost. At present there is alack of commercially viable technology for long duration type ofelectricity storage except for pumped hydro. However, pumped hydro islimited by availability of suitable lands due to geologicalenvironmental constrains.

Metal-air, particularly zinc-air, electrochemical systems have been seenas promising technologies for low cost large scale energy storage. Therehave been continuous attempts to develop energy storage systems based onzinc-air chemistry including rechargeable batteries, mechanically andhydraulically rechargeable fuel cells (see review articles by X. G.Zhang: “Zinc Electrodes”, and S. Smedley and X. G. Zhang, “Zinc-Air:Hydraulic Recharge”, in Encyclopedia of Electrochemical Power Sources,Eds. Jungen Garche etc., Amsterdam: Elsevier, 2009).

Electrically rechargeable zinc-air batteries have high energy density.The main technical issues have been fast degradation of thebi-functional air cathode and the detrimental change of the morphologyof zinc anode during cyclic discharging and charging. Numerousdevelopment efforts have been made to resolve these technicalchallenges. Some recent developments can be appreciated from the USpatent applications, for example, US2010/0021303 and US2010/0316935.

For zinc-air fuel cells, the zinc active anode material is like fuel andcan be generated and regenerated by electro deposition. The generationof zinc material by electro deposition serves the function of storingelectricity. The deposited metallic material together with electrolytein fluidic form is fed or fueled into the fuel cells, which serves thefunction of generating electricity from the stored energy in themetallic zinc. Regenerative zinc fuel cells are ideal for economicallong duration energy storage for three fundamental reasons: 1) powergeneration and energy storage are separated such that energy can bestored independently at low cost; 2) zinc has a high energy density,highest among the common metals that can be reduced in aqueouselectrolytes and 3) zinc is inexpensive, one of the lowest cost metalsin the market.

Regenerative zinc-air fuel cell systems have many advantages overrechargeable battery systems such as independent scaling of power andcapacity and continuous discharging without interruption for charging.Many development efforts have been made on zinc fuel cell technology ascan be appreciated in the patent literature, for examples, U.S. Pat.Nos. 5,434,020, 5,849,427, 6,706,433 and US Patent ApplicationUS2010/330437. The main technical challenges have been clogging orjamming during fuelling or transporting the zinc materials into and outthe electrochemical cells and uneven distribution of the materialswithin a cell and between the cells. It is essential to have solutionsto resolve these technical problems for zinc air fuel cell to functionreliably and efficiently.

Metal-redox flow batteries, particularly zinc-redox flow batteries, areanother technology system that has been considered having the potentialfor low cost energy storage. Redox couples of bromine, cerium and ironhave been used for development of zinc-redox flow battery technologies,as indicated in literature: Progress in Flow Battery Research andDevelopment (by M. Skyllas-Kazacos et al in Journal of TheElectrochemical Society, Vol. 158 (8) R55-R79), 2011, US 2013/0252062A1, U.S. Pat. No. 8,293,390, and U.S. Pat. No. 5,607,788. As well,iron-redox flow battery has also been explored as disclosed in US20140065460 A1. However, in the current designs of metal-redox flowbatteries the capacity of the batteries is limited by the thickness ofthe metal anodes. It will be advantageous if the capacity of themetal-redox flow batteries is not limited by the thickness of metalanodes and thus the energy capacity can be scaled independent of powergeneration.

FIGURES

These and other features of the preferred embodiments of the inventionwill become more apparent in the following detailed description in whichreference is made to the appended drawings wherein:

FIG. 1a A schematic illustration of the basic elements and structure ofthe electrochemical cell according to an embodiment of the presentinvention where the charging assembly is above of the dischargingassembly in the same housing.

FIG. 1b A schematic illustration of the gear mechanism for mobilizingthe wipers in the charging assembly.

FIG. 1c A schematic perspective and cross sectional illustration of thestructure of the oxygen cathode in the discharging assembly.

FIG. 1d A schematic perspective illustration of some of the possiblestructures of the oxygen cathode in the discharging assembly.

FIG. 2a A schematic illustration of the basic elements and structure ofthe electrochemical cell including electrolyte and deposited metalmaterials (same as shown in FIG. 1 with omission of some elements forsimplicity)

FIG. 2b A schematic illustration of the electrochemical cell system inwhich the cathodes in the charging assembly have a plurality of discreteactive surface areas for metal deposition.

FIG. 2c A schematic illustration of a charging cathode with a pluralityof discrete areas for deposition of metal;

FIG. 2d A schematic illustration of the cathode of FIG. 2c taken alongthe lines A-A.

FIG. 2e A schematic illustration of the charging assembly in which theelectrodes are in a cylindrical form

FIG. 2f A schematic illustration of the electrochemical system having astirring mechanism in the anode spaces in the discharging assembly.

FIG. 2g A schematic illustration of the electrochemical system having abaffle between the oxygen cathodes in the discharging assembly

FIG. 3a A schematic illustration of the basic elements and structure ofthe electrochemical cell viewed from the plane and along the lines C-Cin FIG. 1.

FIG. 3b A schematic illustration of the electric terminals and leads forthe discharging assembly and the inlet and outlet for air to the oxygencathodes that are positioned through the sides of the cell container.

FIG. 4 A schematic illustration of the elements and structure of theelectrochemical cell from the plane and along the lines B-B in FIG. 1.

FIG. 5 A schematic illustration of the basic elements and structure ofthe electrochemical cell viewed from the plane and along the lines A-Ain FIG. 1.

FIG. 6 A schematic illustration of an electrochemical cell in which thecharging assembly is beside of the discharging assembly in the samecontainer.

FIG. 7 A schematic illustration of the electrochemical system withmultiple cells in one container; each cell has the basic elements andstructure shown in FIG. 1.

FIG. 8 a and b A schematic illustration of an electrochemical cell thathas the same structure of that shown in FIG. 1 with a chamber beneaththe discharging assembly, (a) view from one side and (b) view with aright angle from the side illustrated in (a).

FIG. 8 c A schematic illustration of an embodiment with a baffle betweenthe oxygen cathodes

FIG. 8 d, A schematic illustration of an embodiment with a plurality ofchambers for electrolyte circulation through the metallic materialthrough the space between individual pair of oxygen cathodes.

FIG. 8 e A schematic illustration of an embodiment with tubes positionedbetween the oxygen cathodes; the tubes have a plurality of holes alongthe length for passing through electrolyte.

FIG. 9a A schematic illustration of an electrochemical cell that has achamber beside the discharging assembly.

FIG. 9b A schematic illustration of an electrochemical cell that has achamber beneath that is extended to beside the discharging assembly.

FIG. 10 A schematic illustration of the electrochemical cell shown inFIG. 8 having a separate tank for containing extra electrolyte.

FIG. 11 A schematic illustrations of multiple cells in one containerwith a chamber beneath each cell; there are only one charging cathodeand one oxygen electrode in each cell. (The various components, such aspipes, conducting elements motor etc that are illustrated in otherfigures such as FIG. 1 and FIG. 8 are omitted for clarity.)

FIG. 12 a and b A schematic illustration of a cell with one oxygenelectrode and one pair of charging electrodes in a single container (a);and with one pair of charging electrodes and two oxygen electrodesmounted on the side of the cell container (b).

FIG. 13 A schematic illustration of an embodiment of the electrochemicalsystem with a plurality of cells for energy storage and generation.

FIG. 14 a and b A schematic illustration of power profiles for (a)concurrent charging and discharging (b) and alternating charging anddischarging

FIG. 15 A schematic illustration of power profiles of concurrentcharging and discharging with a varying input power during charging andconstant output power during discharging.

FIG. 16 a and b A schematic illustration of a cell containing thecharging assembly (a) and a cell containing the discharging assemblies(b).

FIG. 16c A schematic illustration of a discharging cell in which thereis a chamber beneath the charging assembly for electrolyte and thedischarging oxygen cathodes are in a triangular shape.

FIG. 17 a and b A schematic illustration of an embodiment of (a) a setof discharging cells are integrated with a charging cell and (b)multiple sets of discharging cells are integrated with a charging unit.

FIG. 18 a and b A schematic illustration of an operation of theelectrochemical cell system where the metal deposit is generated in thecharging cells (a), stored in storage containers (b) which may betransported to the discharging cells (c) that are located in differentplaces.

FIG. 19 A schematic illustration of the basic elements and structureelectrochemical cell according to an embodiment of the presentinvention, in which the oxidant is in liquid form such as bromine forthe positive electrodes.

FIG. 20 A schematic illustration of the basic elements and structure ofthe electrochemical cell viewed from the plane and direction E-E asindicated in FIG. 19.

FIG. 21 A schematic illustration of an embodiment of the electrochemicalsystem shown in FIG. 19 with an external tank for storing the liquidreactant that is circulated in and out of the electrochemical cell bypumps.

FIG. 22 A schematic illustration of an embodiment of the electrochemicalsystem having a compartment in the cell container for containing theliquid reactant for reactions involved with the positive electrodes.

FIG. 23 Current and voltage as a function of time for the prototype testcell measured during charging and discharging.

SUMMARY OF INVENTION

The present invention provides an electrochemical system, apparatus andmethods for storing electricity in metals. According to a general aspectof the invention, it is an electrochemical cell system comprising acharging assembly or device for metal deposition, a discharging assemblyor device for metal dissolution, and a mean for containing a metal. Theelectrochemical system further comprises means of containment for thecharging assembly, discharging assembly, electrolyte and metallicmaterial. The charging and discharging assemblies can be containedseveral ways and can be operated for various types of charging anddischarging functions involved in electrical energy storage.

In another general aspect of the present invention, it provides a methodfor generating and storing electricity comprising generating a metallicmaterial in a charging assembly by electro-metal deposition, a storagefacility for the metallic material, and dissolving the metallic materialin discharging assembly to generate electricity. The method furthercomprising means for transport or movement of the metallic material andelectrolyte, and means of containment for the charging assembly,discharging assembly, electrolyte and metallic material.

In one aspect of the invention, the discharging assembly of theelectrochemical system comprises at least one cathode with the spaceadjacent to the cathode for containing metallic material as the anode.The cathode and anode form an electrode couple by which dischargingprocesses occur. The space for containing the anode can also bedescribed as the space below the at least one discharging cathode or thespace amid the cathode and the interior surface of the housing or thespace amid the cathodes if there are a plurality of cathodes.

In another aspect of the invention, the charging assembly of theelectrochemical cell system consists of at least one anode and cathodecouple for electro deposition of a metallic material on the surface ofthe cathodes, and a mechanism to dislodge or remove the depositedmetallic material on the cathodes.

In another aspect of the invention, the electrochemical cell systemcomprises two sets of redox reactions, one set involving a metal andanother involving a fluid or gaseous reactant. The oxidation andreduction reactions for the metal occur on the negative electrodes,which are the cathodes in the charging assembly and the anodes in thedischarging assembly, and the oxidation and reduction reactions of afluid or gaseous reactant occur on the positive electrodes, which arethe anodes in the charging assembly and cathodes in the dischargingassembly.

In one embodiment, a discharging assembly and a charging assembly arehoused in the same body of electrolyte in a single container to form acell. The discharging assembly can be located underneath of the chargingassembly or on the side of the charging assembly. The metallic materialformed from deposition in the charging assembly is transported or movedinto the anode spaces or anode beds in the discharging assembly bygravity if the charging assembly is above the discharging assembly or bya mechanical means such as a pump if they located side by side. Thedischarged metal material is dissolved in the electrolyte which istransported or moved from the discharging assembly to the chargingassembly through concentration homogenization of the electrolyte bydiffusion and convection. A space or head room is above the dischargingassembly for containing extra metallic material when the anode spaces inthe discharging assembly are filled.

In another aspect, the system may further comprise aspects, for example,a chamber in proximity to the discharging assembly or a tube beneath theanode beds for electrolyte circulation through the anode beds betweenthe oxygen cathodes, a stirring mechanism in the anodes beds to improvepacking density and uniformity of the metallic material, a bafflebeneath the anode beds to help direct the metallic material toward thesurface of the oxygen cathode.

In another embodiment, a plurality of discharging assemblies and aplurality of charging assemblies are contained in a plurality ofcompartments in a container to form a plurality of cells in thecontainer.

In another embodiment the charging and discharging assemblies arelocated in separate containers forming a charging cell and a dischargingcell. The metallic material and electrolyte are transported between thecharging and discharging cells by a mechanical means such as pumps. Thecharging cell or cells may be located in proximity and are connectedwith discharging cell or cells with pipes; alternatively the chargingcells and discharging cells may be disconnectedly located in differentlocations. The independent discharging cells can be used in applicationsas motive or back-up power sources. The independent charging cells canbe located in places close to the sources of primary energy such windand solar. The deposited metallic materials generated in the chargingcells and be contained and shipped to the discharging cells located indifferent places.

As a further embodiment, in addition to separated charging anddischarging cells, metallic material and electrolyte can also becontained in separated containers or reservoirs, which contain noelectrodes and thus are beneficial for low cost storage and transport.

In a preferred embodiment of the present invention, the metal is zincfor the reactions on the negative electrodes and the reactant is oxygenfor the reactions on the positive electrodes. The functionality of thisembodiment had been experimentally demonstrated, the result beingdisclosed in this document.

In one aspect of the preferred embodiment, the oxygen cathode is astructure that has a cavity inside for passing air or an oxygencontaining gas through and its exterior surfaces exposed in theelectrolyte. The oxygen cathode can be independently removed from thedischarging assembly. The structure may consist of a frame covered withan oxygen membrane electrode to form a cavity defined by the frame andthe membrane electrodes, and an inlet and outlet for the passage ofoxygen or air in and out of the cavity. The shape of the oxygen cathodesmay be planar, circular, triangular, oval etc.

In another aspect of the proffered embodiment, the reactant for theredox reactions on the positive electrodes may be associated with iron,cerium, bromine, chlorine, chromium, vanadium and other elements, ofwhich the redox reaction has a potential positive to that of zinc.

In another aspect of the invention, the electrochemical system is aregenerative metal fuel cell in which the metallic material, as thefuel, generated from electro deposition in the charging assembly, isloaded (or fueled, or fed, or moved) into the spaces between thepositive electrodes of the discharging assembly and the dischargedmaterial is carried out the discharging assembly through diffusion andconvection.

In another aspect of the invention, the electrochemical system is like aflow battery in which the reactions for the positive electrodes involvea redox couple in a fluid or gaseous form that flow through the positiveelectrodes of the charging and discharging assemblies.

In further aspect of the invention, the electrochemical system is like agenerator, or a reactor or a plant capable of generating electricitycontinuously and on demand by feeding materials through and thedischarged material can be regenerated in the same system which resultsin energy storage.

The present invention in essence is about storing electricity inmetallic materials that are not bound in the electrode structures likebattery in which the active materials are permanently fixed in thestructures of electrodes. The basic principle of the invention has ageneral applicability allowing for designing electrochemical energystorage systems with different chemistries, cell structures andoperations. It has many advantages over other energy storagetechnologies for many potential applications.

The electrochemical system of the present invention, due to its inherentadvantages of using metallic materials for electricity storage, may beused for various energy storage applications that are not feasible withbatteries. One particular feature of the present invention that isdifferent from conventional batteries is that the system may be used asan electrical energy storage and power source at the same time such thatit may be used to provide a continuous and stable electrical power in anon-stopping manner. Since the cells of the electrochemical system cancontain active material outside of the structures of electrodes, thecapacity of energy storage using the system can be flexibly varied atlow costs. Also, the embodiment with separate charging and dischargingfacilities may be used for applications with distributed power sources.Furthermore, storage of only metallic materials but not the electrodesand other components in simple plastic containers may allow electricitystorage for long terms at low cost.

DETAILED DESCRIPTION

An exemplary embodiment of the electrochemical cell according to theprinciples of the present invention uses oxidation and reduction ofoxygen in the air and of a metal as the electrochemical reaction couple,of which the basic elements and structure are illustrated in FIG. 1 etal to FIG. 5. FIG. 1a is a schematic illustration of the electrochemicalcell without electrolyte and metal. FIG. 2a is a schematic illustrationof the electrochemical cell shown in FIG. 1a having electrolyte anddeposited metal materials. FIGS. 3a , 4 and 5 are the schematicillustrations viewed from different cross sectional planes anddirections indicated in FIG. 1 a.

As shown in FIGS. 1a and 2a the electrochemical cell 100 includes acharging assembly 200 (roughly outlined by the dashed line), adischarging assembly 300 (roughly outlined by the dashed line), anelectrolyte 400, a container 110 and a number of auxiliary componentswhich will be described in the following paragraphs.

The charging assembly 200 is located on the top section of the container110 above the discharging assembly. The charging assembly is in a space102 (second space) above the discharging assembly. The charging assemblyconsists of at least one or a plurality of charging cathodes 230 andanodes 220, (only two cathodes and three anodes are illustrated in thefigures for simplicity). The charging cathodes and anodes areappropriately spaced to match to the layout of the discharging assembly300 which will be described further below. The cathodes and anodes ofthe charging assembly are physically secured on the horizontal bars 271and 272. Bar 271 is secured onto the container 110 through an attachmentfixture 270, for example and not limited to a screw or aperture. Thecathodes and anodes may alternatively be mounted directly on the cellcontainer 110. The cathodes comprise of a conductive material 231, forexample and not limited to magnesium, that is stable in the electrolyteand has low adhesion to the deposited metallic material. The edges ofthe cathodes are covered by an insulating material 232, for example andnot limited to polymeric materials, to prevent metal deposition on theedges. As a variation, the cathode may comprise a plurality of discreteactive surface areas as illustrated in FIG. 2b for generating discretemetal deposits. FIGS. 2c and d is an illustration of an example of sucha cathode with discrete deposition areas 231 separated by insulatingmaterial 232.

In the embodiment illustrated in FIG. 1a , the layout of the electrodesof the charging assembly is in parallel to the electrodes of thedischarging assembly. Alternatively, it may be structured such that theelectrodes of the charging assembly are at perpendicular or at someother angles relative to the electrodes of the discharging assembly.

The mechanism for removing the deposited metallic material compriseswipers 260 mounted on a shaft 250 which is horizontally positioned withend two plates 210 and 210 a through the middle of the chargingassembly. The rotating motion of the shaft 250 is enabled with a motor280 through a worm gear mechanism having worm gear elements 240, gears241, gear shaft 242 and a support base fixture 243 as illustrated inFIG. 1b . Gear 241 is mounted on shaft 250 and gear 240 on a fixture 243mounted on the end plate 210. The shaft 250 is preferably not inphysical contact with the cathodes and anodes to minimize frictionalresistance; the holes in the middle of the cathodes and anodes arelarger than the diameter of the shaft. Alternatively, instead ofrotating wipers, wipers that either moving horizontally or verticallymay be used for dislodging the metal deposits from the cathodessurfaces. As a further alternative, the cathodes can be moved relativeto the wipers that are fixed. Further alternative embodiments mayinclude other mechanisms such as shaking or vibration the chargingcathodes for removing the metal deposits.

As an alternative embodiment, the cathode and anode pairs of thecharging assembly can be in a cylindrical form as illustrated in FIG. 2e. For the electrode pair 1000, the cylindrical cathode 1012 with currentlead 1014 is outside of the cylindrical anode 1011 with current lead1013. In operation, the metal deposits can be periodically removed withwiper 1015. As in the case of planer shape of charging cathodes, thecylindrical form of charging cathodes can also have discrete activesurface areas for metal deposition.

During charging operation the metal in the electrolyte is reduced on thesurfaces of the cathodes forming metal deposit 501 as illustrated atFIG. 2a . As the deposits grow on the cathode surface, they areperiodically dislodged by wipers 260 from the surfaces and transportedby gravity downward into first space 101 (anode beds) between the oxygencathodes of the discharging assembly 300 underneath the chargingassembly. The metal deposits may pile up into second space 102 tovariable heights above of the discharging assembly after the first spaceis filled. The first space may also be described as that below the topedges of the oxygen cathodes or that amid of the oxygen cathodes and theinterior surface of the container for the case where the shape of theoxygen cathodes is non-planar as shown in FIG. 1 d.

The electrical current of the cathodes of the charging assembly isconducted to terminal 290 via leads 291 of the cathodes and bus 292. Thecurrent of the anodes is conducted to terminal 295 via leads 296 of theanodes and bus 297. The portion of leads 291 that is immersed inelectrolyte is covered with an insulating material 291 a (shown in FIGS.2c and d ), such as a polymer coating or film to prevent metaldeposition on the leads.

For the embodiment shown in FIG. 1a , the discharging assembly 300,located beneath of the charging assembly comprises one or a plurality ofoxygen cathodes 301 (discharging cathodes) with first space 101 for, asillustrated at FIGS. 1a and b , containing anodes 500 (discharginganodes) consisting of the deposited metallic material 501 fallen fromthe charging assembly. Above the anodes pile 502 in the second space isthe metallic material in excess of that in the anode beds (first space).The current of the anodes is collected by anode current collectors 330(see FIG. 1a ), on the bottom of cell 100, and 331 (see FIG. 3) on theside of the anode beds and is conducted through a horizontal bus 332 anda lead 333 to terminal 334 outside of the cell on the top (see FIGS. 1aand 3). The anode current collectors can be made of copper or othermetal alloys and may also vary in size and shape and be placed atdifferent locations in the anode spaces. The current of the oxygencathodes is conducted to terminal 323 on top of the container viaelectrical leads 321 of individual oxygen cathodes, bus 320 and lead322. All surface areas of the current conducting elements for thecathodes, i.e. 320, 321, and 322, that are submerged in the electrolyteis covered with an insulating material or the insulating material toprevent possibility of contact between cathodes and the metallicmaterial. Alternatively, the electrical leads of the dischargingassembly may be connected to the terminals on the side of the cellcontainer as illustrated in FIG. 3 a.

The anodic electrode (negative electrode) of the discharging assemblymay be considered as consisting of one anode when all the metallicmaterial in the anode beds in the first space is a continuous body andconsidered as consisting of a plurality of anodes when the anode bedsare only partially filled by the metallic material with the embodimentin FIG. 1 a.

The discharging assembly of the electrochemical system may also comprisea stirring mechanism 601, which for example may be a rod or a bar,inserted in the discharging anode for higher packing density and betterdistribution of the metallic materials in the anode as shown in FIG. 2f. The stirring mechanism can be powered by the same motor that powersthe whipping mechanism 280 through extension 602 or alternatively by anindependent power source such as a motor, compressed air or compressedfluid. The stirring mechanism, depending on the specific design, maygenerate linear, angular, rotational or vibration movement. Thedischarging assembly, as shown in FIG. 2g , may further comprise abaffle 603 between the oxygen cathodes to direct the metallic materialtoward the surface of the cathodes as the material moves downward duringdischarging. The baffle may be made of plastic material or a conductivematerial such as a metal, in the case of which the conductive materialmay also serve as the current collector for the discharging anode.

The oxygen cathode 301 in the discharging assembly of the embodimentshown in FIG. 1a is a planar structure with a cavity 302 as illustratedin FIG. 1 c. The oxygen cathode comprises a frame 306 covered with twomembrane oxygen electrodes 303 that are permeable to air but isimpermeable to water. The surfaces of the oxygen cathodes are coveredwith a separator 304 to prevent direct contact between the cathodes andanodes. The oxygen cathode may alternatively be in non-planar structureswith examples illustrated in FIG. 1 d. The cavity 302 within the cathodeis for holding air or oxygen or a gas containing oxygen to allow thereduction of oxygen. The cavity is completely sealed except for an inletand an outlet to allow air or gas passing through. The air is suppliedinto the cavities of the oxygen cathodes by an air pump (not shown inthe figures) that is located, as shown at FIG. 3, external of theelectrochemical cell via inlet 312, manifold 311 and tubes 310 andleaving the cavity via tubes 310 a, manifold 311 a and outlet 312 a onthe top of the container 110. It may be beneficial that tubes 310 and310 a and electric lead 321 (shown at FIG. 1c ) are bundled together ormade into a single element for simplifying the structure. Alternatively,air or oxygen may be conducted to the oxygen cathode through the side ofthe cell container via inlet our outlet 313 and 313 a as shown in FIG.3b . The oxygen membrane electrode 303 is supported with a corrugatedboard 305 (see FIG. 1c ) to prevent yielding of the membrane electrodeunder the pressure from the surrounding electrolyte.

The oxygen cathode of such design has the advantage of allowingindependent removal of individual oxygen cathode without affecting othercathodes in the discharging assembly, and thus allowing convenientchanging of cathodes or cleaning of the cell container when needed. Italso has the advantage of maintaining the discharging function of thesystem when electrolyte leakage occurs in one oxygen cathode when thereis a plurality of cathodes in the discharging assembly.

The cell container 110 (or tank) can be made of plastic materials.Preferably, the container is made of a continuous piece of plasticmaterial with no discontinuity, such as holes and gaps, exists below thesurface 401 (see FIG. 6) of electrolyte such that there is nopossibility of electrolyte leakage to outside of the cell. This is aparticular advantage over the conventional designs of metal-air cells,in which the sides of cell container are covered by air electrodes andare prone to leaking of electrolyte. On cover 120 of the container,there is a gas outlet with filter 420 (see FIG. 1a ) to retain theelectrolyte in the mist, containing mainly oxygen, generated during theoperation of the system. There may be also catalytic material disposedin the filter 420 for recombination of the small amount of hydrogen thatmay be generated during the operation of the system as a side reaction.On the cover 120 there may also have other elements such as terminalsfor electrical conduction, air inlet and outlet, a motor or an air pump.The dimension and shape of the container 110 is determined according tothe actual designs of the charging and discharging assemblies. Theheight of the cell container can be varied to change the space 102(second space) without affecting the structures of the charging anddischarging assemblies of the cell. This flexible variation of thesecond space that change the volume between the charging and thedischarging assemblies allows for variation of energy storage capacitieswith only marginal impact on the manufacturing and cost of the cell. Asmetallic material can be contained in the second space to form pile 502(see FIG. 2a ) above the discharging assembly, the cell can have a largestorage capacity or long runtime.

During the discharging operation of the cell, the anodes 500 areconsumed as the metal deposit is dissolved and the dissolved metal inthe electrolyte is transported out of the anode spaces with electrolytevia diffusion and convection and returns to the charging assembly. Thematerial in pile 502 above the anodes falls into the anode spaces as thesolid anode material is consumed, which maintains the electrochemicalactivity of the anodes.

An alternative embodiment is to house the charging assembly and thedischarging assembly side by side as illustrated in FIG. 6. Thecompartment of charging assembly and the compartment of the dischargingassembly is separated by a divider 111 which is permeable to electrolyteand allows passing of electrolyte but not permeable to solid metalmaterial such that the electrolyte is shared in both compartments. Themetal deposits formed on the side of charging assembly is moved to theside of discharging assembly by pump 1201 through pipes 1202 and 1203.In the embodiment illustrated in FIG. 6, the electrodes of the chargingassembly are parallel to the electrodes of the discharging assembly.Alternatively, it may be structured such that the electrodes of thecharging assembly are perpendicular or in some other angle relative tothe electrodes of the discharging assembly.

Another alternative embodiment is to have more than one cell in a singlecontainer as illustrated in FIG. 7, where three cells are contained inone container. Cells 1, 2 and 3, each comprise a charge assembly anddischarging assembly, and each is separated by a wall 112 which isimpermeable to electrolyte such that there is no electrochemicalinterference between the cells. The cells in this embodiment can beconnected in series to give a higher voltage of the system contained inthe container. This embodiment may also have the advantage of sharingthe motion mechanism, through a motion transmission device 281 and shaft282, needed for removal of deposits on the cathodes of the chargingassemblies in the cells. The same construction may be just one cell withmultiple compartments separated by walls through which or over whichelectrolyte can pass.

An alternative embodiment is to comprise a mechanism to circulate theelectrolyte within the system. One mechanism for circulating electrolyteis to add a chamber that is in proximity, adjacent, next or close to thefirst space. FIGS. 8a and b shows the embodiment of the electrochemicalsystem with a chamber 103 below the discharging assembly. The chamber isseparated from the first space in the discharging assembly by aseparator or a filter material 1101 that is supported by a perforatedplate 1102. In operation the electrolyte can be circulated by a pump1105 via pipes 1104 and 1106 among the first space, the second space andthe chamber in either direction (in FIG. 8a direction of flow asindicated by 1007 and 1007 a is from the second space to the first spaceto the chamber). Alternatively, as shown in FIG. 8d , there areplurality of chambers which are separated by a wall 606, each chambercorresponding to one pair of the discharging cathodes such that theelectrolyte may circulate through the anode area between each pair ofthe oxygen cathodes through manifold 607, tubing 608 and pump 1005. As afurther variation, instead individual chambers electrolyte circulationfor the corresponding anode spaces can be accomplished using a pipe 609with holes 610 along its length placed in each anode bed as illustratedin FIG. 8 e.

The electrolyte circulation as a forced convection can help the processof concentration homogenization of the electrolyte in differentlocations within the cell and can improve the performance of theelectrochemical system particularly at high current densities. At highcurrent densities, the metal concentration may be depleted near thecathode surfaces of the charging assembly during charging and may behighly concentrated in the anode spaces between oxygen cathodes of thedischarging assembly during discharging. Electrolyte circulation canhelp increase the metal concentration near the cathode surfaces of thecharging assembly and remove the dissolved metal in the dischargingassembly.

As a further variation, as shown in FIG. 8c there is a baffle between604 the oxygen cathodes that separates the first space and the chamber.The electrolyte can be circulated between the first space and thechamber through gaps 605 at the lower end of the baffle, which have thebenefit of having the electrolyte flow path closer to the dischargingcathode surfaces where the concentration of the dissolved zinc ishigher.

The chamber 103 may also be positioned beside of the first space andsecond space as illustrated in FIG. 9a where the chamber is separated bya wall 112 from the first and second spaces except for a section ofareas beside the discharging assembly where electrolyte is allowed topass through. Alternatively, the chamber may also be extended to theside as illustrated in FIG. 9b ; the relatively large size of thechamber can be advantageous when more electrolyte is desirable forextended storage capacity.

The further variation of the embodiment is illustrated in FIG. 10 wherean independent and detachable tank 110 a is connected with cellcontainer 110 with pipe 1008 and joints 1009 and 1010 to store extraelectrolyte for additional and optional energy storage capacity. Theelectrolyte in tank 110 a and in the cell container 110 can becirculated by pump 1105 via pipes 1104 and 1106.

The embodiment with electrolyte circulation can also be used in a systemwhere multiple cells are places in a single container as illustrated inFIG. 11. In FIG. 11 there is only one cathode in the charging assemblyand one oxygen cathode in the discharging assembly.

It is also possible for a system to have only on charging cathode andone charging anode and one oxygen cathode in container 110 asillustrated in FIG. 12a (the other components including pump, pipes, andanode current collector is omitted for simplicity). As a furthervariation, a single cell may have only two oxygen electrodes 303 mountedon side opening of container 110 as illustrated by FIG. 12b , whichallows the direct access of oxygen in the air without having to pump airthrough into the system.

The active metal for the reactions in the electrochemical cell systemmay be zinc, aluminum, magnesium, lead, and iron and their alloys. Themetal or alloy may be further alloyed with other elements such asindium, bismuth, tin, gallium, antimony, calcium and cadmium forcontrolling hydrogen side reaction or morphology of the metal deposits.

The electrolyte may be an aqueous solution made of soluble chemicals ofincluding but not limited to solutions of chlorides, sulfates,phosphates, hydrochloric acid, sulfuric acid, sodium hydroxide,potassium hydroxide and lithium hydroxide.

Depending on the active metal and electrolyte, the conductive material231 of the cathodes of the charging assembly may be graphite, carbon,magnesium, aluminum, stainless steel, titanium and zirconium. Theinsulating material 232 may be plastics or ceramics. The anodes 220 ofthe charging assembly may be made of carbon, graphite, stainless steel,steel, titanium alloys, zirconium alloys and nickel alloys.

In a preferred embodiment, the active metal is zinc. The cathodesubstrate, the conductive material 231, for zinc deposition in thecharging assembly may be made of metals or alloys including but notlimited to magnesium, titanium, zirconium, tantalum graphite, andchromium. The anodes in the charging assembly 220 may be made of metalsand alloys including but not limited to steels, carbon, graphite,stainless steels, titanium, and nickel alloys. The electrolyte may beaqueous solutions of potassium hydroxide, sodium hydroxide or lithiumhydroxide and is preferably potassium hydroxide. The concentration ofpotassium hydroxide solutions may range between 10 to 45%. Zinc has ahigh solubility in concentrated potassium solutions, about 1 molar at35% KOH, and can form supersaturated solutions 2 to 3 times of thenormal solubility, allowing storage of high content of potential energyin the solutions. The zinc metallic material may be alloyed with one ormore other elements including but not limited to aluminum, magnesium,tin, bismuth, indium, gallium, lead, antimony and cadmium.

As a preferred active metal, zinc has a unique set of technical andeconomical attributes including low equilibrium potential, goodelectrochemical reversibility, fast reaction kinetics, large overpotential for hydrogen reaction, good conductivity, low equivalentweight, high specific energy, high volumetric energy density, abundance,low cost, low toxicity, and ease of handling (X. G. Zhang, Corrosion andElectrochemistry of Zinc, Springer and Zinc Electrodes, Encyclopedia ofElectrochemical Power Sources, Elsevier). These attributes make zinc afavorable anode material for electrochemical power sources since theinvention of battery two hundred years ago.

The good electrochemical reversibility and fast reaction kinetics meanzinc can dissolve and deposit readily near its equilibrium potential.The large over potential for hydrogen reaction means that zinc is stablein aqueous solutions and a high current efficiency during deposition.

In a zinc-oxygen cell, zinc dissolves to form zincate ions duringdischarge and zincate ions are reduced to form metal deposit duringcharge according to the following equation:Zn+4OH⁻=Zn(OH)₄ ²⁻+2e E₀=−1.25VConcurrently, oxygen is reduced during discharge and hydroxyl ions areoxidized during charge according to the following equation:O₂+2H₂+4e=4OH⁻ E₀=0.4 VThe overall reaction in the cell isZn+O₂+4OH⁻=Zn(OH)₄ ²⁻ E₀=1.65V

In the embodiments of the present invention, zinc metal is deposited onthe cathodes in the charging assembly. The deposited metallic zincmaterial is dislodged from the surface of the cathode periodicallythrough a mechanical means such as wipers. The cathode substratematerial for zinc deposition may be magnesium, titanium, zirconium,tantalum and their alloys or conductive substrates coated with thesemetals or alloys, on which the metal deposits may be easily removed bywipers. As a preferred embodiment the cathode for zinc deposition ismade of magnesium or its alloys.

In a particular embodiment, the cathode 230 for zinc depositioncomprises a plurality of discrete active surfaces made of conductivematerial 231. The discrete surfaces, on which metal is deposited, areisolated by insulating material 232 as indicated FIGS. 2c and 2d . Thematerial deposited on such electrode can be more uniformly distributedin the anode spaces in the discharging assembly.

The electrochemical cell system of the present invention can be used asan electrical storage system and a power source with variable storageand power capacity by connecting together individual cells asillustrated in FIG. 13, where a group of cells are in series connection.Individual cells or groups of cell series can also be connected inparallel depending on the design requirements for output voltage andcurrent etc. One particular novel feature of the present invention isthat the system can be used as an electrical energy storage and a powersource at the same time, that is concurrent charging and discharging orsimultaneously, which is not possible with conventional batteries. FIGS.14a and b show two charging and discharging profiles, wherein thecharging and discharging are continuous with time in FIG. 14a , but arealternating with time in FIG. 14b . The system of the present inventioncan function with both profiles while in contrast conventional batteriescan only function with the alternating charging and discharging profile.

The concurrent charging and discharging can be used for many potentialapplications that are not possible with conventional batteries. Forexample, the system of present invention can allow continuouslyconverting unstable power, such as solar or wind power, into a stablepower as illustrated in FIG. 15. Furthermore, it allows for full use ofenergy sources such as wind and solar without interruption unlike aconventional battery which needs to be discharged once it is fullycharged.

As a variation of the present invention, the electrochemical system canalso be designed for the charging and discharging assemblies to locatein separate containers for independent charging and discharging cells asillustrated in FIGS. 16a and b . The independent discharging cells andindependent charging cells provide a range of possible applications thatare not feasible for the embodiment with charging and dischargingassemblies in the same container. As a varied embodiment, thedischarging only cell (without charging assembly) has a chamber inproximity to the discharging assembly for electrolyte circulation asillustrated in FIG. 16c . As well, use of triangularly shaped oxygencathodes 301 a in this embodiment makes the removal of dischargedmaterial easier; the content may be poured out by turning the containersideway or upside down.

In one embodiment, one or more of the discharging units (each may have agroup of cells) can be integrated with a charging unit (can viewed ascentralized metal deposition), which may consist of one or a pluralityof cells, as shown in FIG. 17a . The metallic material and electrolytein the charging unit 100 b and the discharged material in thedischarging cells 100 a can be transported via a reservoir 100 c throughpipes and pumps 710, 711, 720, 721, 730 and 731. The charged materialfrom the charging unit 100B which may have one or more discharging cellscan also be pumped to a plurality of strings of discharging units asillustrated in FIG. 17b . The centralized deposition or electroplatingmay bring operational benefits for large scale systems, similar toelectrowinning plants in the metal refining industry, which may beviewed as plants for large scale energy storage.

In another embodiment, the charging units and discharging units can belocated in different locations for certain applications, for example, asconceptually illustrated in FIGS. 18a, c (path 1). The discharging unitscan be used as back-up power sources or power sources for mobile devicessuch as vehicles. The discharging units after being fully discharged canthen transported back to the location of the charging units for removingthe discharged material and refill with fresh metallic material. Foreasy removal of the discharged material the oxygen cathodes in thedischarging cell may be tapered, such as triangular shape, as shown inFIG. 1 d and FIG. 16c . Alternatively, instead of transporting thedischarging unit back and forth, only the charged and dischargedmaterials are transported using containers 100 c between the locationsfor charging and discharging (FIGS. 18a, b, and c path 2). Transportingonly the active materials in containers without the electrodes and theassociated components can greatly reduce the complexity and cost of thetransportation.

The option of using simple containers to contain only the activematerials also allows to store energy economically for long times, i.e.days, weeks, or even months. It is obvious that to store only low costmaterials (for example zinc and KOH solutions) in low cost containers(made of e.g. plastics), have a great cost advantage over other types ofenergy storage such as batteries which generally have a complexstructure. This potential application may have a significant implicationon the future growth of renewable energy; as large scale of electricitystorage for long times (days, weeks, or months) would become essentialin the future when a large portion of society's electricity is generatedby weather dependent energy sources such as solar and wind.

The cell having only the discharging assembly can also have the optionof using materials that are not electro deposited, that is, that areproduced by metallurgical or mechanical means. In the case of zinc,particulate materials such as zinc powder or zinc pellets produced bythermal spraying or casting can be used as the active anode material inthe discharging cells in the discharging only cells. It may be operatedby mechanically filling or loading the cell with fresh anode materialand electrolyte and removing out (pouring or pumping) the dischargedmaterial after discharging. The embodiment of the discharging cellconsisting of triangular oxygen cathodes (shown in FIG. 1d ) allowseffective loading and emptying the discharging cell. Furthermore, such adischarging only cell allows the use of the metals that is not feasibleto be reduced electrochemically in aqueous solutions. In particular, theembodiment of the cell with only the discharging assembly allows the useof aluminum and magnesium, which have much higher energy densities thanzinc but are not effectively reducible in aqueous solutions. Inoperation, anode material in the form of particulates such as powders orpellets can be loaded together with electrolyte, either separately or asa mix, into the discharging cell. The electrolyte after discharging canbe pumped out or pour out of the cell and the cell is ready for addingfresh material and electrolyte. This embodiment of using aluminum ormagnesium has the advantage in applications as mobile power sources forwhich high energy density is an important requirement.

FIGS. 19 and 20 schematically illustrates another embodiment of thepresent invention which allows the use of liquid form of reactantsinstead of gaseous form like oxygen. Redox couples that may be suitablefor use in this embodiment includes Br₂/Br²⁻, Fe²⁺/Fe³⁺, Ce³⁺/Ce⁴⁺,VO²⁺/VO₂ ⁺, and other redox couples that have a potential positive tothat of zinc. The chemical agents of the redox couples can be dissolvedin a suitable electrolyte with sufficient quantities and thus can betransported in a fluidic form.

As a specific embodiment, for example, the redox couple for thereactions on the positive electrodes is based on bromine and themetallic material is zinc, that is, it is a zinc-bromine chemistry. Thereactions for this embodiment can be represented as follows (P. C.Butler et al, Zinc/Bromine Batteries in Handbook of Batteries, McGrawHill):Negative electrode Zn−2e=Zn²⁺ E⁰=0.763VPositive electrode Br₂+2r=Br⁻ E⁰=1.087VTotal reaction Zn+Br₂=ZnBr₂ E⁰=1.85V

The electrochemical system using zinc-bromine reactions consists of twoelectrolytes, a negative electrolyte containing ZnBr and a positiveelectrolyte containing Br₂/Br⁻. The two electrolytes are physicallyseparated in order to prevent direct reaction between zinc and bromine.The negative electrolyte is stored inside the cell container 110. Thepositive electrolyte is stored in a tank 900 and is circulated in andout of the cell with pumps and pipes 912 and 922 as illustrated in FIG.21. The size of the electrolyte tank for the positive electrolyte mayvary depending on number of cells it connects with and the capacity ofthe cells.

For the embodiment illustrated in FIGS. 19 and 20, during charge zinc isdeposited on the cathodes of the charging assembly while bromine ions inthe electrolyte flowing through anode chambers 363 are reduced onelectrodes 361. During discharge the zinc is oxidized into zinc ions inthe discharge assembly while the bromine in the positive electrolyteflowing through the chambers 353 of the cathodes in the dischargingassembly is reduced on electrodes 351. To separate the negativeelectrolyte and positive electrolyte, a separator or ionic selectivemembrane 352 and 362 covers the surfaces of the anodes in the chargingassembly and the cathodes in the discharging assembly. The positiveelectrolyte is circulated through the anodes in the charging assemblyvia manifold (375), inlet (378) and outlet (378 a); it is circulatedthrough the cathodes of the discharging assembly via manifold (371),inlet (373) and outlet (373 a). The two sets of inlets and outlets areconnected via pipes (931, 931 a, 932, and 932 a) and valves (912 and922) to an electrolyte container 900. As an alternative embodiment, theelectrolyte for the positive electrode, that is, that containing brominecan be contained for each cell by adding a compartment 104 on the cellcontainer as illustrated in FIG. 22. It is to be noted that although itis not particularly exemplified for the zinc-bromine system all thealternative embodiments and possible variations described andillustrated for the system involving oxygen as the reactant for thepositive electrodes may also be applicable the zinc-bromine system.

The embodiment of the present invention for using redox reactions ofbromine as the reactions for the positive electrodes has a big advantageover the current design of zinc-bromine flow batteries in which thecapacity is limited by the thickness of the zinc electrode. The chargingcapacity and discharging capacity of the electrochemical system of thepresent invention is not limited by the thickness of the deposit on thecathode of the charging assembly neither by the thickness of the anodeof the discharging assembly. Another advantage with the presentinvention is that the operation is insensitive to the morphology of themetal deposit and it allows the formation non-uniform deposits of zincmetallic material on the cathodes of during charging; the formation ofnon-uniform deposits is detrimental for the zinc-bromine batteries ofthe current designs.

The present invention has significant advantages over prior arts onmetal fuel cells including at least: 1) it resolves the challengingproblems relating to feeding metallic materials into individual cellsand removing discharged material out of cells without clogging orjamming; 2) it allows the oxygen cathode to be constructed as a selfcontained component, like an air cartridge allowing air to pass through,and can be independently removed from the discharging assembly. It thusallows convenient removal of individual air cathodes for service andmaintenance without affecting the integrity of the cell; and 3) itallows the use a container made of single continuous piece of plasticmaterial to contain all elements that are in touch with electrolyteinside the container, which removes the possibility of potentialelectrolyte leaking out the cell. In comparison to conventionalbatteries, the electrochemical system of the present invention has theadvantages of: 1) it can perform concurrent charging and dischargingfunctions; 2) it allows large capacities and flexible and low costcapacity scaling; 3) it allows charging and discharging to be operatedat different locations; and 4) it allows energy storage for long timesat low cost as on the active materials (without electrodes) can bestored in simple plastic containers. The present invention canpotentially be used in a wide range of applications including but notlimited for: 1) economical storage of renewable energy such as solar andwind; 2) improving the stability and efficiency of electrical grid; 3)as the storage device for off-grid or micro grid distributed powersource systems; 4) as back up or UPS power sources: 5) as power sourcesfor mobile applications; and 6) back up long term electricity storagefor emergency situations and for situations when there is interruptionof electricity supply from renewable energy sources due to bad weather.

The working principle and functionalities of the present invention arefurther demonstrated by the following example. The example and theirparticular details set forth herein are presented for illustration onlyand should not be construed as a limitation on the claims of the presentinvention.

Example(s)

A cell was constructed according to the embodiment schematicallyillustrated in FIG. 2b . The cell container, made of Plexiglas, has aninterior dimension of 24 cm in length, 13 cm in width and 50 cm inheight. The charging assembly had one cathode and two anodes. The anodeswere flat sheets of stainless steel of 1 mm in thickness. The activesurface of cathode was made of pure magnesium with a plurality ofdiscrete active surface areas of 5 mm×5 mm that were separated by 5 mminactive zones. The inactive zones and the edges of the cathode werecovered with epoxy resin. The dimension of the cathode was 21 cm×21 cm.The total number of discrete active areas was 632 for the two sides anda total area of a cathode was 158 cm². The distance between the cathodeand anodes was 1 cm. The charging assembly was mounted on the cellcontainer with bars made of a plastic material Acetal and the top edgeof the assembly is 6 cm from the top of the container. The wipers weremade of plastic material Derin. The wipers were mounted on thehorizontal draft made of stainless steel, which was mechanically joinedto a set of drive worm gears which was connected to a motor mounted ontop of the cell container.

The discharging assembly had three air cathodes that were spaced for 2.5cm to form two anode spaces. The cathode in the middle had membraneoxygen electrode on both sides of the surfaces while only one membraneelectrode on the two end cathodes. The cathode had a dimension of 22cm×12 cm×1 cm with a 20 cm×10 cm×0.9 cm cavity sealed within thecathode. The active surface area on each side of the cathode is 200 cm².The cathode had a frame made of Plexiglas and the membrane oxygenelectrodes were glued on the frame. The membrane oxygen electrode wasobtained from Reveo Inc, NY, United States. The membrane oxygenelectrode was mechanically joined to a strip of stainless steel that ledto the outside of the cell to serve as the current conductor. Thesurfaces of oxygen cathodes and the stainless strips were covered with aseparator material (FS2227E produced by Freudenberg Nonwovens L.P, NC,United States). There was an opening on each end of the cathode and theopenings were joined with vinyl tubes for passing air which was suppliedwith an air pump. A copper strip, a part of which was laid on the bottomof each anode space in the discharging assembly, serves as currentcollector for the zinc anode. The electrolyte was 34% KOH containing0.5M of zinc oxide. The anode spaces of the discharging assembly werefilled with zinc deposits.

The cell was tested using a battery testing equipment. FIG. 23 shows theresults of two 10 hours cycles of charging and discharging. This exampledemonstrated that the electrochemical cell system of the presentinvention can be reduced to practice.

The above description and illustrated embodiments have been provided toillustrate the basic structural and functional principles of the presentinvention and shall not be interpreted to be limiting. It is apparentthat those with skills in the art who review this disclosure willreadily see the various possible combinations, changes and modificationsin the structure, parts, elements, materials, arrangements, andfunctionality without departing from the spirit and scope of the presentinvention. Accordingly, any modifications and equivalents that can bereadily conceived from the teaching of this document should beconsidered falling within the scope of the present invention specifiedin the following claims.

The invention claimed is:
 1. An electrochemical cell system, comprising:a housing; an electrolyte disposed in the housing; a metallic material;a plurality of charging anodes and a plurality of charging cathodes atleast partially immersed in the electrolyte; a plurality of dischargingcathodes immersed in the electrolyte; and a plurality of first spacesadjacent the discharging cathodes, wherein: the housing is a singlecontainer and the plurality of charging cathodes, the plurality ofcharging anodes, the plurality of discharging cathodes and the pluralityof discharging anodes are all housed within the single container; thecharging cathodes and charging anodes are above the dischargingcathodes; the metallic material is electrochemically deposited on thecharging cathodes during charging; the metallic material deposited onthe charging cathodes is at least intermittently dislodged; the metallicmaterial, when positioned in the first spaces, forms a plurality ofdischarging anodes; and the metallic material is electrochemicallydissolved during discharging.
 2. The electrochemical cell system ofclaim 1, further comprising a second space above the dischargingcathodes for storing the excess metallic material when the first spacesare filled.
 3. The electrochemical cell system of claim 1, wherein theelectrolyte is at least intermittently circulated for homogenizing theconcentration of the electrolyte.
 4. The electrochemical cell system ofclaim 1, wherein the portion of the housing in contact with theelectrolyte is impermeable to air.
 5. The electrochemical cell system ofclaim 1, wherein the metallic material comprises a metal selected fromthe group consisting of zinc, aluminum, magnesium, lithium, iron,cadmium, lead, tin, bismuth, indium, and antimony or an alloy of themetal.
 6. The electrochemical cell system of claim 1, further comprisinga chemical agent for the electrochemical reactions on the charginganodes and the discharging cathodes, and the chemical agent is selectedfrom the group consisting of oxygen, bromine, chlorine, iron salts,vanadium salts, chromium salts, titanium salts, and cerium salts.
 7. Theelectrochemical cell system of claim 1, wherein the metallic material isdislodged by wiping, or scraping, or shaking, or vibration, or theircombinations.
 8. The electrochemical cell system of claim 1, wherein themetallic material, when dislodged from the charging cathodes, moves bygravity into the first spaces.
 9. The electrochemical cell system ofclaim 1, further comprising a chamber in fluid communications with thefirst spaces through a filtering material.
 10. The electrochemical cellsystem of claim 1, wherein: each of the discharging cathodes and thecharging anodes comprises an electrode within a chamber comprising aseparator; and the electrolyte is a negative electrolyte for reactionsinvolving the deposition and dissolution of the metallic material. 11.The electrochemical cell system of claim 10, further comprising apositive electrolyte, a reservoir for containing the positiveelectrolyte, and a pump for circulating the positive electrolyte betweenthe chamber and the reservoir.
 12. The electrochemical cell system ofclaim 1, wherein the discharging cathode comprises: one or more oxygenmembrane electrodes; a cavity enclosed by the oxygen membraneelectrodes; one or more separators covering the surface of the oxygenmembrane electrodes; and an inlet and an outlet for passing air or anoxygen-containing gas into and out of the cavity.
 13. Theelectrochemical cell system of claim 1, further comprising a baffle ineach first space for directing the metallic material and the electrolytetoward the surfaces of the discharging cathodes.
 14. The electrochemicalcell system of claim 1, wherein deposition of the metallic materialduring charging and dissolution of the metallic material duringdischarging are carried out at the same time.
 15. An electrochemicalcell system, comprising: a housing; an electrolyte disposed in thehousing; one or more oxygen cathodes immersed in the electrolyte and oneor more first spaces between the oxygen cathodes; a metallic material,when positioned in the first spaces, forms one or more discharginganodes; and one or more charging anodes and one or more chargingcathodes at least partially immersed in the electrolyte; wherein: thehousing is a single container and the one or more charging cathodes, theone or more charging anodes, the one or more oxygen cathodes and the oneor more discharging anodes are all housed within the single containerthe metallic materials is deposited on the charging cathodes duringcharging; the metallic material is at least intermittently dislodgedfrom the charging cathodes; the charging cathodes and charging anodesare above the discharging cathodes; a second space between (a) thedischarging cathodes and (b) the charging cathodes and charging anodesfor containing the metallic material when the first spaces are filled;each of the oxygen cathodes comprises a cavity enclosed by one or moreoxygen membrane electrodes for containing air or oxygen-containing gas;the metallic material is dissolved during discharging; and theelectrolyte is circulated at least intermittently.
 16. A method forgenerating and storing electricity using the electrochemical cell systemaccording to claim 1, the method comprising: storing electricity byelectrochemical deposition of the metallic material with a chargingassembly comprising the plurality of charging cathodes and the pluralityof charging anodes at least immersed in the electrolyte contained in thehousing; dislodging the metallic material deposited on the chargingcathodes; placing the metallic material in the plurality of first spacesbetween the plurality of discharging cathodes, which forms a dischargingassembly at least partially immersed in the electrolyte, wherein themetallic material in the first spaces forms the plurality of discharginganodes; containing the metallic material in a second space above thedischarging assembly when the first spaces are full; generatingelectricity by electrochemical dissolution of the metallic material inthe discharging assembly; and circulating the electrolyte within thehousing.
 17. The method of claim 16, wherein the storing electricity andthe generating electricity occur simultaneously by carrying out thedeposition of the metallic material and the dissolution of the metallicmaterial at the same time.
 18. The electrochemical cell system of claim11, wherein the positive electrolyte comprises bromine.